JP2020186360A - Production apparatus and production method of bio-emulsion fuel using vegetable oil - Google Patents
Production apparatus and production method of bio-emulsion fuel using vegetable oil Download PDFInfo
- Publication number
- JP2020186360A JP2020186360A JP2019105429A JP2019105429A JP2020186360A JP 2020186360 A JP2020186360 A JP 2020186360A JP 2019105429 A JP2019105429 A JP 2019105429A JP 2019105429 A JP2019105429 A JP 2019105429A JP 2020186360 A JP2020186360 A JP 2020186360A
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- Prior art keywords
- oil
- water
- mixed
- catalyst
- bioemulsion
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000000446 fuel Substances 0.000 title claims abstract description 60
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 45
- 235000015112 vegetable and seed oil Nutrition 0.000 title claims abstract description 37
- 239000008158 vegetable oil Substances 0.000 title claims abstract description 37
- 239000000839 emulsion Substances 0.000 title abstract description 11
- 239000003921 oil Substances 0.000 claims abstract description 263
- 235000019198 oils Nutrition 0.000 claims abstract description 262
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 170
- 239000003054 catalyst Substances 0.000 claims abstract description 135
- 238000012546 transfer Methods 0.000 claims description 31
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 17
- 239000012535 impurity Substances 0.000 claims description 13
- 238000003756 stirring Methods 0.000 claims description 10
- 239000000377 silicon dioxide Substances 0.000 claims description 7
- 235000012239 silicon dioxide Nutrition 0.000 claims description 7
- 229910052613 tourmaline Inorganic materials 0.000 claims description 7
- 229940070527 tourmaline Drugs 0.000 claims description 7
- 239000011032 tourmaline Substances 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 3
- 229910021536 Zeolite Inorganic materials 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052732 germanium Inorganic materials 0.000 claims description 3
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 claims description 3
- 229910052744 lithium Inorganic materials 0.000 claims description 3
- 239000011777 magnesium Substances 0.000 claims description 3
- 229910052749 magnesium Inorganic materials 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- 239000000741 silica gel Substances 0.000 claims description 3
- 229910002027 silica gel Inorganic materials 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 3
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 3
- 239000010457 zeolite Substances 0.000 claims description 3
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 239000002803 fossil fuel Substances 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 5
- 239000000701 coagulant Substances 0.000 abstract description 4
- 239000000654 additive Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 230000000996 additive effect Effects 0.000 abstract 1
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 239000010779 crude oil Substances 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 229910052604 silicate mineral Inorganic materials 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 229910001571 halide mineral Inorganic materials 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
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- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/14—Injection, e.g. in a reactor or a fuel stream during fuel production
- C10L2290/141—Injection, e.g. in a reactor or a fuel stream during fuel production of additive or catalyst
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/22—Impregnation or immersion of a fuel component or a fuel as a whole
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/38—Applying an electric field or inclusion of electrodes in the apparatus
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/544—Extraction for separating fractions, components or impurities during preparation or upgrading of a fuel
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/547—Filtration for separating fractions, components or impurities during preparation or upgrading of a fuel
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/58—Control or regulation of the fuel preparation of upgrading process
Abstract
Description
本願は、植物油を用いたバイオエマルジョン燃料製造装置及び製造方法に関するものである。 The present application relates to a bioemulsion fuel production apparatus and a production method using vegetable oil.
最近の化石燃料の枯渇問題や温室効果ガスの発生の問題が世界的に大きな問題となっている。 The recent problems of fossil fuel depletion and greenhouse gas generation have become major problems worldwide.
この問題を解決するための発明に関連して、特許文献1(発明の名称:燃料の製造方法)には、水と軽油、灯油や重油など燃料油をそれぞれ磁力が印加される領域に供給してこれらを微粒化して混合することにより、汎用性が高く、微粒化が可能であり、安定した状態を持ったエマルジョン燃料を製造する方法及び装置が開示されている。 In relation to the invention for solving this problem, Patent Document 1 (title of the invention: method for producing fuel) supplies water and fuel oil such as light oil, kerosene and heavy oil to regions where magnetic force is applied. A method and an apparatus for producing an emulsion fuel which is highly versatile, can be atomized, and has a stable state by atomizing and mixing these are disclosed.
しかし、このような従来の燃料の製造方法及び装置は、燃料がエマルジョンの形態を持っているので、水−オイルの分離が起こりオイルの成分が残ってしまう。したがって、引火点の大幅な上昇と発熱量の低下が起こり、化石燃料の消費量を大幅に削減することができないという問題点があった。 However, in such conventional fuel production methods and devices, since the fuel has an emulsion form, water-oil separation occurs and the oil component remains. Therefore, there is a problem that the flash point is significantly increased and the calorific value is decreased, and the consumption of fossil fuel cannot be significantly reduced.
このような問題点を解決するために、本発明者が出願した特許文献2(発明の名称:改質燃料の製造装置及び製造方法)は、水タンク部に超音波やプラズマ電界を印加し、水を微粒化し、酵素タンクを介して酵素を供給し、過酸化水素を分解することで、水とオイルが簡単に混合することができて、流水の分離が起こらず、エマルジョンの形態を持つ改質燃料の問題点である引火点の上昇、発熱量の低下などの問題点を解消した。 In order to solve such a problem, Patent Document 2 (title of the invention: a reformed fuel manufacturing apparatus and manufacturing method) filed by the present inventor applies ultrasonic waves or a plasma electric field to a water tank portion. By atomizing water, supplying the enzyme through the enzyme tank, and decomposing hydrogen peroxide, water and oil can be easily mixed, running water does not separate, and the invention has the form of an emulsion. Problems such as an increase in the ignition point and a decrease in calorific value, which are problems with quality fuel, have been resolved.
しかし、このような従来の改質燃料製造装置及び製造方法は、プロセスが複雑で、酵素タンクを使用して酵素を管理するのが困難で、超音波や電場を印加する構成の構造が複雑であるため製作するのに費用が多く発生し、メンテナンスなどが大変であるという問題点があった。 However, in such a conventional reformed fuel manufacturing apparatus and manufacturing method, the process is complicated, it is difficult to control the enzyme using the enzyme tank, and the structure of the configuration in which ultrasonic waves or electric fields are applied is complicated. Therefore, there is a problem that it costs a lot to manufacture and maintenance is difficult.
実際にシステムを生産し、販売する過程において、それぞれの国ごとに、化石燃料に添加する添加剤が異なりかつ水の性質に違いがあり、それに相当する触媒を状況に合わせて作ることが困難であるという現実的な問題が発生した。 In the process of actually producing and selling the system, the additives added to fossil fuels are different and the properties of water are different in each country, and it is difficult to make a corresponding catalyst according to the situation. There was a real problem of being there.
本願は、それぞれ国ごとの添加剤を使用する化石燃料を使用せずに、簡単に入手できる植物油を原料に使用したバイオエマルジョン燃料を製造することを目的とする。 An object of the present application is to produce a bioemulsion fuel using easily available vegetable oil as a raw material without using fossil fuels that use additives for each country.
上記技術的課題を達成するための技術的手段として、本明細書の第1番目の例示による植物油を用いたバイオエマルジョン燃料製造装置は、流入されたオイルを保存し、不純物を除去して精製された油を準備するオイルタンク部;流入した水を水タンク触媒を利用して前処理する水タンク部;上記オイルタンク部と上記水タンク部に接続されて、オイルタンク部から流入された精製された油と、水タンク部から流入した前処理された水を攪拌して混合油を形成する混合油生成部;前記混合油生成部と接続されて、前記混合油生成部から流入した混合油をイオン化触媒を利用して、バイオエマルジョン燃料に最終生成するイオン化触媒部を含むことができる。 As a technical means for achieving the above technical problems, the bioemulsion fuel production apparatus using the vegetable oil according to the first embodiment of the present specification is refined by storing the inflowed oil and removing impurities. Oil tank section that prepares oil; Water tank section that pretreats the inflowing water using a water tank catalyst; Purified that is connected to the oil tank section and the water tank section and flows in from the oil tank section. A mixed oil generating section that stirs the oil and the pretreated water that has flowed in from the water tank section to form a mixed oil; the mixed oil that is connected to the mixed oil generating section and flows in from the mixed oil generating section. The ionization catalyst can be utilized to include an ionization catalyst portion that is finally produced in the bioemulsion fuel.
上記技術的課題を達成するための技術的手段として、本明細書の第2番目の例示による植物油を用いたバイオエマルジョン燃料の製造方法は、オイルタンク部内に供給されたオイルから凝集剤と遠心分離型デカンタを利用して不純物を除去して、精製された油を準備する段階;水タンク部内に供給された水を水タンク触媒により前処理して、前処理された水を準備する段階;混合油生成部内で、上記のオイルタンク部から流入された精製された油と、上記水タンク部から流入した前処理された水を攪拌して混合油を形成する段階;イオン化触媒部内で、前記混合油生成部内から流入した前記混合油をイオン化触媒を利用して、最終的に、バイオエマルジョン燃料を生成することができる。 As a technical means for achieving the above technical problems, the method for producing a bioemulsion fuel using vegetable oil according to the second example of the present specification is to centrifuge from the oil supplied into the oil tank portion with a flocculant. The stage of preparing refined oil by removing impurities using a mold decanter; the stage of pretreating the water supplied into the water tank with a water tank catalyst to prepare the pretreated water; mixing A step of stirring the refined oil flowing from the oil tank section and the pretreated water flowing from the water tank section to form a mixed oil in the oil generating section; the mixing in the ionization catalyst section. The mixed oil that has flowed in from the oil generation section can be finally produced as a bioemulsion fuel by using an ionization catalyst.
前述した本願の課題解決手段によれば、植物油を用いたバイオエマルジョン燃料は、燃焼時、既存の化石燃料を使用したエマルジョン燃料よりも、同じ容積より高いカロリーを発生し、既存の化石燃料を使用したエマルジョン燃料の短所を補完する役割をする。 According to the above-mentioned problem-solving means of the present application, the bioemulsion fuel using vegetable oil generates higher calories than the emulsion fuel using the existing fossil fuel when burned, and uses the existing fossil fuel. It serves to complement the shortcomings of fossil emulsion fuels.
植物油を用いたバイオエマルジョン燃料は、エマルジョン燃料と同じ特徴的な公害物質の排出低減効果を持つ。 Bioemulsion fuel using vegetable oil has the same characteristic emission reduction effect of pollutants as emulsion fuel.
植物油を用いたバイオエマルジョン燃料は、植物油の豊富な供給先の確保を通じ、化石燃料を利用したエマルジョン燃料比、生産単価を大幅に下げることができる利点がある。 Bioemulsion fuel using vegetable oil has the advantage that the ratio of emulsion fuel using fossil fuel and the production unit price can be significantly reduced by securing abundant supply destinations of vegetable oil.
下記には、添付した図面を参照して、本願が属する技術分野で通常の知識を有する者が容易に実施できるように、本願の実施例を詳しく説明する。しかし、本願明細書では、さまざまな異なる形態で具現されることがあり、ここで説明する実施例に限定されない。そして図面で本願を明確に説明するために説明と関係ない部分は省略し、明細書全体を通じて類似した部分については同様の符号を付した。 Hereinafter, examples of the present application will be described in detail with reference to the accompanying drawings so that a person having ordinary knowledge in the technical field to which the present application belongs can easily carry out the implementation. However, the specification of the present application may be embodied in various different forms, and is not limited to the examples described herein. In order to clearly explain the present application in the drawings, parts unrelated to the description are omitted, and similar parts are designated by the same reference numerals throughout the specification.
本願明細書全体では、いくつかの部材が他の部材の「上」に位置するとき、これはどのような部材が他の部材に接しているだけではなく、両方の部材の間に別の部材が存在する場合も含む。 Throughout the specification of the present application, when some members are located "above" other members, this is not only what member is in contact with the other member, but another member between both members. Including the case where.
本願明細書全体では、どの部分がどのような構成要素を「含む」とするとき、これは特に反対される記載がない限り、他の構成要素を除外するのではなく、他の構成要素をさらに含むことができることを意味する。本願明細書全体で使用される用語「約」、「実質的に」などは言及された内容に固有の製造及び油質の許容誤差が提示されるときに、その数値またはその数値に近いこととして使用され、本願書の理解を得るために正確で絶対的な数値が記載されている開示内容を非良心的な者が不当に利用することを防ぐために使用される。本願明細書全体で使用される用語「〜(する)段階」または「〜の段階」は「〜のための段階」の意味ではない。 In the entire specification of the present application, when what part "contains" what component, this does not exclude other components unless otherwise stated, but further other components. Means that it can be included. The terms "about", "substantially", etc. used throughout the specification of the present application are defined as being or close to that value when the manufacturing and oil quality tolerances specific to the referred content are presented. It is used to prevent unscrupulous use of disclosures that are used and contain accurate and absolute numbers to gain the understanding of this document. The terms "step" or "step" as used throughout the specification do not mean "step for".
以下、添付された図面を参照して、本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
まず、本願の実施例による植物油を用いたバイオエマルジョン燃料製造装置(10)(以下、「本バイオエマルジョン燃料の製造装置(10)」について説明する。 First, the bioemulsion fuel production apparatus (10) using the vegetable oil according to the embodiment of the present application (hereinafter, “the present bioemulsion fuel production apparatus (10)” will be described.
図1(a)、1(b)、1(c)をにおいて、本バイオエマルジョン燃料の製造装置(10)と関連する構成について説明する。 The configuration related to the bioemulsion fuel production apparatus (10) will be described with reference to FIGS. 1 (a), 1 (b), and 1 (c).
図1に示すように、本製造装置(10)は、オイルタンク部(100)、水タンク部(200)、混合油生成部(300)、及びイオン化触媒部(400)を含んでいる。 As shown in FIG. 1, the manufacturing apparatus (10) includes an oil tank section (100), a water tank section (200), a mixed oil generating section (300), and an ionization catalyst section (400).
オイルタンク部(100)は、オイル供給ポンプ(110)からの植物油を供給することができる。供給された植物油は、オイルタンク(120)に一時的に保存することができる。植物油は、燃焼時に発電機やエンジンのパフォーマンスを悪化させる不純物を含んでいるので、バイオエマルジョン燃料を生成する前に、これを除去しなければならない。したがって、オイルタンク部(100)には、不純物を凝集、凝固させる凝集剤をオイルタンク(120)に投与するための凝集剤投入機(130)が含まれる。オイルタンク(120)のオイルはオイル移送ポンプ(140)を介して遠心分離型デカンタ(150)に移送される。遠心分離型デカンタ(150)は、高速で回転しながら凝固された不純物と精製された油を分離する役割をする。精製されたオイルは、オイル収集タンク(160)に一時保存され、精製油移送ポンプ(180)を介して精製オイルタンク(170)に送られる。 The oil tank portion (100) can supply vegetable oil from the oil supply pump (110). The supplied vegetable oil can be temporarily stored in the oil tank (120). Vegetable oils contain impurities that degrade the performance of generators and engines when burned and must be removed before producing bioemulsion fuels. Therefore, the oil tank portion (100) includes a coagulant input machine (130) for administering a coagulant that agglomerates and coagulates impurities to the oil tank (120). The oil in the oil tank (120) is transferred to the centrifuge decanter (150) via the oil transfer pump (140). The centrifuge decanter (150) is responsible for separating solidified impurities from refined oil while rotating at high speed. The refined oil is temporarily stored in the oil collection tank (160) and sent to the refined oil tank (170) via the refined oil transfer pump (180).
水タンク部(200)は、流入した水を水タンク触媒を用いて前処理する。水タンク部(200)は、水供給ポンプ(210)からの水を供給することができる。 The water tank section (200) pretreats the inflowing water using a water tank catalyst. The water tank section (200) can supply water from the water supply pump (210).
混合油生成部(300)は、オイルタンク部(100)と水タンク部(200)とに接続される。混合油生成部(300)は、オイルタンク部(100)から流入した精製された油と、水タンク部(200)から流入した前処理された水をインラインミキサー(360)を使用して混合油を形成する。 The mixed oil generating section (300) is connected to the oil tank section (100) and the water tank section (200). The mixed oil generating section (300) uses an in-line mixer (360) to mix the refined oil flowing from the oil tank section (100) and the pretreated water flowing from the water tank section (200). To form.
具体的には、精製オイルタンク(170)にある精製された油は、高圧オイル移送ポンプ(310)を介してインラインミキサー(360)に移送される。また、水タンク(220)の前処理された水は、高圧水移送ポンプ(320)を介してインラインミキサー(360)に移送される。それぞれの移送管には移送量を調整することができる開閉弁(330a、330b)が設置されている。開閉弁(330a、330b)の開度に応じて精製された油と前処理された水の混合割合が決定される。精製された油と前処理された水の割合は、一般的には1:1を基準にするが、状況に応じて、6:4または7:3の割合で混合することができる。また、それぞれの移送管には圧力計(340a、340b)と流量計(350a、350b)が設置されており、精製された油と前処理された水の圧力と流量をリアルタイムで測定することができる。これによりオイルと水の量を制御部(main controller)(図示せず)で正確に監視し、制御することにより、混合原油の割合を正確に調節することができる。 Specifically, the refined oil in the refined oil tank (170) is transferred to the in-line mixer (360) via the high pressure oil transfer pump (310). Further, the pretreated water in the water tank (220) is transferred to the in-line mixer (360) via the high-pressure water transfer pump (320). On-off valves (330a, 330b) that can adjust the transfer amount are installed in each transfer pipe. The mixing ratio of refined oil and pretreated water is determined according to the opening degree of the on-off valves (330a, 330b). The ratio of refined oil to pretreated water is generally 1: 1 but can be mixed in a ratio of 6: 4 or 7: 3, depending on the situation. In addition, pressure gauges (340a, 340b) and flowmeters (350a, 350b) are installed in each transfer pipe to measure the pressure and flow rate of refined oil and pretreated water in real time. it can. This allows the proportion of mixed crude oil to be accurately adjusted by accurately monitoring and controlling the amounts of oil and water with a main controller (not shown).
インラインミキサー(360)を介して物理的に混合された混合油は混合油タンク(370)に移送され、一時的に保存される。 The mixed oil physically mixed via the in-line mixer (360) is transferred to the mixed oil tank (370) and temporarily stored.
イオン化触媒部(400)は、混合油生成部(300)と接続される。具体的にはイオン化触媒部(400)は、混合油タンク(370)から流入した混合油をイオン化触媒を用いて、最終的にバイオエマルジョン燃料を生成する。 The ionization catalyst section (400) is connected to the mixed oil generating section (300). Specifically, the ionization catalyst unit (400) finally produces a bioemulsion fuel by using the mixed oil flowing from the mixed oil tank (370) using the ionization catalyst.
図2を用いて、本願の実施例によるオイルタンク(120)について詳細に説明する。 The oil tank (120) according to the embodiment of the present application will be described in detail with reference to FIG.
オイルタンク(120)は、オイル導入ライン(121)、オイルヒーター(122)、オイル水位測定器(123)、エアベント(124)、オイル攪拌機(125)、及びオイル出口ライン(126)を含んでいる。 The oil tank (120) includes an oil inlet line (121), an oil heater (122), an oil water level meter (123), an air vent (124), an oil stirrer (125), and an oil outlet line (126). ..
オイル導入ライン(121)は、外部からのオイル供給ポンプ(110)を介してオイルタンク(120)の内部にオイルが供給されるラインである。 The oil introduction line (121) is a line in which oil is supplied to the inside of the oil tank (120) via an oil supply pump (110) from the outside.
オイルヒーター(122)は、凝集剤が植物性油内にある不純物をよく凝集することができるように理想的な温度を維持するために設置されている。例示的に、不純物を凝固させるための理想的な温度は50℃である。 An oil heater (122) is installed to maintain an ideal temperature so that the flocculant can well aggregate impurities in the vegetable oil. Illustratively, the ideal temperature for solidifying impurities is 50 ° C.
オイルレベル測定器(123)は、オイルタンク(120)の内部の水位を測定する装置である。 The oil level measuring device (123) is a device for measuring the water level inside the oil tank (120).
オイルレベル測定器(123)を介して測定されたオイルタンク(120)の水位情報は、制御部に伝達することができる。制御部は、このような水位情報をチェックして、オイル供給ポンプ(110)の動作を制御することによりオイルタンク(120)の水位を調節することができる。 The water level information of the oil tank (120) measured via the oil level measuring device (123) can be transmitted to the control unit. The control unit can adjust the water level of the oil tank (120) by checking such water level information and controlling the operation of the oil supply pump (110).
エアベント(124)は、オイルタンク(120)の内部の圧力が高まることを防止するために、内部の空気を外部に放出する管である。 The air vent (124) is a pipe that discharges the air inside the oil tank (120) to the outside in order to prevent the pressure inside the oil tank (120) from increasing.
オイル攪拌機(125)は、オイルタンク(120)の内部でオイルを攪拌する装置であって、いわばオイル攪拌モーターである。例示的に、オイル攪拌モーターはオイルタンク(120)の上部中心に設置されることができる。これらのオイル攪拌機(125)によってオイルが攪拌されることで、オイルの温度が均等に分布、維持することができる。 The oil stirrer (125) is a device that stirs oil inside the oil tank (120), and is a so-called oil stirrer motor. Illustratively, the oil agitation motor can be installed in the upper center of the oil tank (120). By stirring the oil with these oil stirrers (125), the temperature of the oil can be evenly distributed and maintained.
オイル出口ライン(126)は、不純物が凝集されたオイルを、上述された遠心分離型デカンタ(150)に移送するラインである。例示的に、オイルはオイルタンク(120)の下部に装着されたオイル出口調節弁(127)を介してオイル出口ライン(126)に移送することができる。 The oil outlet line (126) is a line for transferring the oil in which impurities are aggregated to the above-mentioned centrifugal decanter (150). Illustratively, oil can be transferred to the oil outlet line (126) via an oil outlet control valve (127) mounted at the bottom of the oil tank (120).
オイル前処理完了は、制御部によって決定されることができる。また、制御部は、オイル出口調整弁(127)の開閉も自動調節することができる。 The completion of oil pretreatment can be determined by the control unit. The control unit can also automatically adjust the opening and closing of the oil outlet adjusting valve (127).
図3を用いて、本願の実施例による水タンク(220)に対して詳細に説明する。 The water tank (220) according to the embodiment of the present application will be described in detail with reference to FIG.
水タンク(220)は、水導入ライン(221)、水位計(222)、水タンク触媒カートリッジ(223)、水攪拌機(224)、及び水出口ライン(225)を含む。 The water tank (220) includes a water inlet line (221), a water level gauge (222), a water tank catalyst cartridge (223), a water stirrer (224), and a water outlet line (225).
水導入ライン(221)は、外部からの水供給ポンプ(210)を介して水タンク(220)の内部に水が供給されるラインである。 The water introduction line (221) is a line in which water is supplied to the inside of the water tank (220) via a water supply pump (210) from the outside.
水位計(222)は、水タンク(220)の内部に収容された水の量(level)を測定する装置である。 The water level gauge (222) is a device that measures the amount of water (level) contained inside the water tank (220).
水位計(222)を介して測定された水タンク(220)の水の量については、制御部に伝達することができる。制御部は、このような水の量についての情報をチェックし、水供給ポンプ(210)の動作を制御することにより、水タンク(220)の水の量、つまり、レベルを調節することができる。 The amount of water in the water tank (220) measured via the water level gauge (222) can be transmitted to the control unit. The control unit can adjust the amount of water in the water tank (220), that is, the level, by checking the information about the amount of such water and controlling the operation of the water supply pump (210). ..
水タンク触媒カートリッジ(223)は、内部に水タンク触媒を備える。これらの水タンクの触媒が水と接触して前処理が行われる。例示的に、水タンク触媒カートリッジ(223)は、水タンク(220)の内部の中心側、つまり中心下部に装着することができる。 The water tank catalyst cartridge (223) includes a water tank catalyst inside. The catalysts in these water tanks come into contact with water for pretreatment. Illustratively, the water tank catalyst cartridge (223) can be mounted on the inner center side of the water tank (220), i.e. at the lower center.
このとき、水タンク触媒はトルマリン原石のようなトルマリン光油を含む第1の水タンク触媒、及び二酸化ケイ素、ケイ酸塩の光油とハロゲン化光油のいずれかを含む第2の水タンク触媒を含むことができる。 At this time, the water tank catalyst is a first water tank catalyst containing tourmaline photooil such as rough tourmaline, and a second water tank catalyst containing either silicon dioxide, silicate light oil or halogenated light oil. Can be included.
例示的に、第2の水タンク触媒は二酸化ケイ素、ケイ酸塩の光油とハロゲン化光油を含む矩形の触媒として利用されることができる。ここで、矩形の触媒は、約1cmの直径を持つことができる。 Illustratively, the second water tank catalyst can be utilized as a rectangular catalyst containing silicon dioxide, silicate light oil and halogenated light oil. Here, the rectangular catalyst can have a diameter of about 1 cm.
これら二つの形態の触媒、つまり第1のタンク触媒と第2の水タンク触媒とを介して水タンク(220)の内部の水は水素に変わり、水の中に含まれている溶存酸素も除去することができる。 The water inside the water tank (220) is converted to hydrogen through these two forms of catalyst, that is, the first tank catalyst and the second water tank catalyst, and the dissolved oxygen contained in the water is also removed. can do.
このように、水タンク(220)には、水タンク触媒の水接触によって前処理された水が形成される。このように前処理された水のpHは、約7.5になることができて、ORP(酸化還元電位)は、約90〜約100で維持されることができる。 In this way, the water tank (220) is formed with pretreated water by the water contact of the water tank catalyst. The pH of the water thus pretreated can be about 7.5 and the ORP (oxidation-reduction potential) can be maintained at about 90 to about 100.
水攪拌機(224)は、水タンク(220)の内部で水を攪拌する装置であって、水攪拌モーターである。例示的に、水攪拌モーターは水タンク(220)の上部中心に設置されることができる。これらの水攪拌機(224)により水が撹拌されることによって、水と水タンクの触媒の接触が最大化されることができる。 The water agitator (224) is a device that agitates water inside the water tank (220) and is a water agitation motor. Illustratively, the water agitation motor can be installed in the upper center of the water tank (220). By stirring the water with these water stirrers (224), the contact between the water and the catalyst in the water tank can be maximized.
水出口ライン(225)は、前処理が完了した水を、後述する混合油生成部(300)に移送するラインである。例示的に、前処理が完了した水は、水タンク(220)の下部に装着された水の出口調節弁(226)を介して水出口ライン(225)に移送することができる。 The water outlet line (225) is a line for transferring the pretreated water to the mixed oil generating unit (300) described later. Illustratively, the pretreated water can be transferred to the water outlet line (225) via a water outlet control valve (226) mounted at the bottom of the water tank (220).
水前処理完了は、制御部によって決定される。また、制御部は、水の出口調整弁(226)の開閉も自動調節することができる。 The completion of water pretreatment is determined by the control unit. The control unit can also automatically adjust the opening and closing of the water outlet adjusting valve (226).
図1(b)を参照し、精製されたオイルと前処理された水が、物理的に混合される混合油生成部(300)に流入される過程についてより詳細に説明する。 With reference to FIG. 1 (b), the process by which the refined oil and the pretreated water flow into the physically mixed mixed oil generator (300) will be described in more detail.
オイルタンク部(100)から精製されたオイルは、精製オイル移送ポンプ(160)を介して精製オイルタンク(170)に流入し、一時的に保存される。精製されたオイルは、再び高圧オイル移送ポンプ(310)を介して高圧の形で移送される。この時、移送されるオイルの量は、開閉弁(330a)によって調節されることができる。また、移送ラインに設置された圧力計(340a)と流量計(350a)とを経て、Y字状のインラインミキサー(360)に流入される。 The oil refined from the oil tank section (100) flows into the refined oil tank (170) via the refined oil transfer pump (160) and is temporarily stored. The refined oil is again transferred in high pressure via the high pressure oil transfer pump (310). At this time, the amount of oil transferred can be adjusted by the on-off valve (330a). In addition, it flows into a Y-shaped in-line mixer (360) via a pressure gauge (340a) and a flow meter (350a) installed in the transfer line.
水タンク部(200)で前処理された水は、高圧水移送ポンプ(320)を介して高圧の形で移送される。この時、移送される水の量は、開閉弁(330b)によって調節されることができる。また、移送ラインに設置された圧力計(340b)と流量計(350b)とを経て、Y字状のインラインミキサー(360)に流入される。 The water pretreated in the water tank section (200) is transferred in the form of high pressure via the high pressure water transfer pump (320). At this time, the amount of water transferred can be adjusted by the on-off valve (330b). In addition, it flows into a Y-shaped in-line mixer (360) via a pressure gauge (340b) and a flow meter (350b) installed in the transfer line.
それぞれの圧力計(340a、340b)と流量計(350a、350b)とは、混合油生成部(300)に供給される精製された油と前処理された水の量を測定する。また、制御部はこれらの測定量に基づいて精製されたオイルと前処理された水の割合を、それぞれの開閉弁(330a、330b)を介して自動的に調節することができる。 The respective pressure gauges (340a, 340b) and flowmeters (350a, 350b) measure the amount of refined oil and pretreated water supplied to the mixed oil generator (300). In addition, the control unit can automatically adjust the ratio of the refined oil and the pretreated water based on these measured amounts via the respective on-off valves (330a, 330b).
このとき、混合油生成部(300)に供給される精製された油の流入量と前処理された水の流入量の比率は、1:1であることが一般的で、状況によっては6:4または7:3の割合も可能なように制御部で事前に設定されている。 At this time, the ratio of the inflow of refined oil supplied to the mixed oil generator (300) to the inflow of pretreated water is generally 1: 1 and may be 6: 1 depending on the situation. It is preset in the control unit so that a ratio of 4 or 7: 3 is also possible.
Y字状のインラインミキサー(360)は、通過する油と水に乱流が発生されるように、内周面に複数の突起が形成される。これらの乱流を介して、油と水の粒子がより多くのムーブメント(movement)を持つようになり、効果的で、物理的な混合ができるようになる。 The Y-shaped in-line mixer (360) has a plurality of protrusions formed on the inner peripheral surface so that turbulence is generated in the passing oil and water. Through these turbulences, oil and water particles will have more movements, allowing for effective and physical mixing.
図4を用いて、本願の実施例による混合油タンク(370)について詳しく説明する。 The mixed oil tank (370) according to the embodiment of the present application will be described in detail with reference to FIG.
本願の混合油タンク(370)は、インラインミキサー(360)を介して物理的に混合された混合油を一時的に保存する場所である。 The mixed oil tank (370) of the present application is a place for temporarily storing the mixed oil physically mixed via an in-line mixer (360).
そのため、混合油タンク(370)は、混合油攪拌機(371)、混合油ヒーター(372)、及び混合油水位計(373)を含むことができる。 Therefore, the mixed oil tank (370) can include a mixed oil stirrer (371), a mixed oil heater (372), and a mixed oil water level gauge (373).
混合油攪拌機(371)は、混合油タンク(370)の内部に流入した混合油が継続的に維持されるように攪拌させる役割をする。例示的に、混合油攪拌機(371)は、上部に位置するモーターと、軸に形成されかつオイルと水とを混合するよう構成されたブレードとを含むことができる。これらのブレードは、混合油を継続的に攪拌することができるように、例えば、約250rpmで回転することができる。 The mixed oil stirrer (371) serves to stir the mixed oil that has flowed into the mixed oil tank (370) so as to be continuously maintained. Illustratively, a mixing oil stirrer (371) can include a motor located at the top and blades formed on the shaft and configured to mix oil and water. These blades can rotate, for example, at about 250 rpm so that the mixed oil can be continuously agitated.
例示的に、混合油タンク(370)内には、混合原油が約5分以内留まり、その間混合油攪拌機(371)の攪拌作業によって、より均一に混合される。 Illustratively, the mixed crude oil stays in the mixed oil tank (370) within about 5 minutes, during which time it is more uniformly mixed by the stirring operation of the mixed oil stirrer (371).
混合油ヒーター(372)は、混合油の温度を一定範囲内に維持させる役割をする。混合油の温度は、25〜35℃に維持されることが望ましい。 The mixed oil heater (372) serves to maintain the temperature of the mixed oil within a certain range. The temperature of the mixed oil is preferably maintained at 25-35 ° C.
混合油水位計(373)は、混合油量(レベル)を測定する役割をする。また、混合油水位計(373)の測定結果は、制御部から継続的に監視し、制御部は、これに基づいて混合油入出口を制御することができる。 The mixed oil water level gauge (373) serves to measure the amount (level) of mixed oil. Further, the measurement result of the mixed oil water level gauge (373) is continuously monitored from the control unit, and the control unit can control the mixed oil inlet / outlet based on this.
図5を用いて、本願の実施例によるイオン化触媒部(400)に関して詳細に説明する。 The ionization catalyst section (400) according to the embodiment of the present application will be described in detail with reference to FIG.
混合油移送ポンプ(405)は、混合油タンク(370)からの混合油を後述するイオン化触媒部(400)に供給する役割をする。例示的に、混合油ポンプ(405)は、混合油の一定量を継続的にイオン化触媒部(400)に供給することができる。また、混合油ポンプ(405)ではトロコイドポンプを使用することができる。 The mixed oil transfer pump (405) serves to supply the mixed oil from the mixed oil tank (370) to the ionization catalyst unit (400) described later. Illustratively, the mixed oil pump (405) can continuously supply a certain amount of the mixed oil to the ionization catalyst unit (400). In addition, a trochoidal pump can be used in the mixed oil pump (405).
イオン化触媒部(400)は、少なくとも一つ以上のイオン化触媒群(410)を含み、イオン化触媒群(410)は、複数のイオン化触媒カートリッジ(411)を含むことができる。 The ionization catalyst unit (400) includes at least one or more ionization catalyst groups (410), and the ionization catalyst group (410) can include a plurality of ionization catalyst cartridges (411).
また、イオン化触媒群(410)は、複数備えられる場合には、互いに直列または並列に接続することができる。ただし、混合原油がイオン化触媒を繰り返し通過できるように、イオン化触媒群(410)は、直列に接続されるか、または直列及び並列の組み合わせで接続することができる。 Further, when a plurality of ionization catalyst groups (410) are provided, they can be connected in series or in parallel with each other. However, the ionization catalyst groups (410) can be connected in series or in a combination of series and parallel so that the mixed crude oil can pass through the ionization catalyst repeatedly.
例示的に、図1(c)及び図5を参照すると、12個のイオン化触媒カートリッジ(411)が直列及び並列の組み合わせで接続されている。より具体的には、例えば、それぞれ3つのイオン化触媒室(411)を有するイオン化触媒群(410)が、4つ備えられており、これらの4つのイオン化触媒群(410)は、図1に示すように、直列及び並列の組み合わせで接続することができる。 Illustratively, with reference to FIGS. 1 (c) and 5, twelve ionization catalyst cartridges (411) are connected in series and in parallel. More specifically, for example, four ionization catalyst groups (410) each having three ionization catalyst chambers (411) are provided, and these four ionization catalyst groups (410) are shown in FIG. As such, they can be connected in series and in parallel.
例えば混合油はイオン化触媒群(410)の引入ラインに設置された開閉弁(406)の開閉に応じて、単一または複数のイオン化触媒カートリッジ(411)を通ることができるように選択することができる。 For example, the mixed oil may be selected so that it can pass through one or more ionization catalyst cartridges (411) depending on the opening and closing of the on-off valve (406) installed in the inlet line of the ionization catalyst group (410). it can.
このように、複数のイオン化触媒群(410)が直列に接続されることにより、混合原油イオン化触媒群(410)を、単一または反復的に通過することになり、混合油をより高い効率でバイオエマルジョン燃料に変換することができる。 By connecting a plurality of ionization catalyst groups (410) in series in this way, the mixed crude oil ionization catalyst group (410) is passed through the mixed crude oil ionization catalyst group (410) singly or repeatedly, and the mixed oil can be passed through the mixed oil with higher efficiency. Can be converted to bioemulsion fuel.
一方、イオン化触媒は、アルミナ、シリカゲル、ゲルマニウム、マグネシア、マグネシウム、酸化チタン、王石、ゼオライト、リチウム鉱、及びバナジウムを主成分として含むことができる。例えば、イオン化触媒カートリッジ(411)は、アルミナ、シリカゲル、ゲルマニウム、マグネシア、マグネシウム、酸化チタン、王石、ゼオライト、リチウム鉱、及びバナジウムを主成分とする球状の触媒が管路に沿って充填される形で備えられている。例示的には、上記触媒の球状の直径は、約1cmである。 On the other hand, the ionization catalyst can contain alumina, silica gel, germanium, magnesia, magnesium, titanium oxide, royal stone, zeolite, lithium ore, and vanadium as main components. For example, the ionization catalyst cartridge (411) is filled with a spherical catalyst containing alumina, silica gel, germanium, magnesia, magnesium, titanium oxide, royal stone, zeolite, lithium ore, and vanadium as main components along the pipeline. It is equipped with. Illustratively, the spherical diameter of the catalyst is about 1 cm.
イオン化触媒カートリッジ(411)は、上記主成分の成分量(成分比)に応じて3種類で分類する。 The ionization catalyst cartridge (411) is classified into three types according to the component amount (component ratio) of the main component.
つまり、イオン化触媒群(410)に含まれる複数のイオン化触媒カートリッジ(411)それぞれは、第1イオン化触媒カートリッジ(411a)、第2イオン化触媒カートリッジ(411b)、及び第3イオン化触媒カートリッジ(411c)を含むことができる。 That is, each of the plurality of ionization catalyst cartridges (411) included in the ionization catalyst group (410) includes the first ionization catalyst cartridge (411a), the second ionization catalyst cartridge (411b), and the third ionization catalyst cartridge (411c). Can include.
例示的に図1と図5を参照すると、イオン化触媒部(400)において、それぞれ3つのイオン化触媒カートリッジ(411a、411b、411c)を有するイオン化触媒群(410)4つは直列及び並列の組み合わせに接続することができる。 Illustratively, with reference to FIGS. 1 and 5, in the ionization catalyst section (400), four ionization catalyst groups (410) each having three ionization catalyst cartridges (411a, 411b, 411c) are combined in series and in parallel. You can connect.
また、混合油は、第1イオン化触媒カートリッジ(411a)、第2イオン化触媒カートリッジ(411b)、第3イオン化触媒カートリッジ(411c)の順でイオン化触媒群(410)を通過する。 Further, the mixed oil passes through the ionization catalyst group (410) in the order of the first ionization catalyst cartridge (411a), the second ionization catalyst cartridge (411b), and the third ionization catalyst cartridge (411c).
例示的に図5を参照すると、混合油はイオン化触媒群(410)を2回繰り返して通過する。つまり、混合油は最初のイオン化触媒群(410)に含まれた第1イオン化触媒カートリッジ(411a)、第2イオン化触媒カートリッジ(411b)、及び第3イオン化触媒カートリッジ(411c)を順次通過した後、これらの最初のイオン化触媒群(410)と直列接続された第二のイオン化触媒群(410)に含まれた第1イオン化触媒カートリッジ(411a)、第2イオン化触媒カートリッジ(411b)、第3イオン化触媒カートリッジ(411c)を再度順次通過する。 Illustratively, with reference to FIG. 5, the mixed oil passes through the ionization catalyst group (410) twice repeatedly. That is, after the mixed oil sequentially passes through the first ionization catalyst cartridge (411a), the second ionization catalyst cartridge (411b), and the third ionization catalyst cartridge (411c) contained in the first ionization catalyst group (410), The first ionization catalyst cartridge (411a), the second ionization catalyst cartridge (411b), and the third ionization catalyst contained in the second ionization catalyst group (410) connected in series with the first ionization catalyst group (410). It passes through the cartridge (411c) again in sequence.
また、第1イオン化触媒カートリッジ(411a)は、混合油内の水に含まれている炭素のイオン化を引き起こす役割をする。 In addition, the first ionization catalyst cartridge (411a) plays a role of inducing ionization of carbon contained in water in the mixed oil.
第2イオン化触媒カートリッジ(411b)は、混合油内の水に含まれる炭素成分と油に含まれる水素の成分を結合させる役割をする。例示的に、混合油内の水に含まれる炭素成分は、第1イオン化触媒カートリッジ(411a)を通過し、イオン化された炭素である可能性がある。また、混合油の油に含まれる水素の成分は、前述したオイルタンク触媒を介してオイルが前処理されることによってイオン化された水素である可能性がある。 The second ionization catalyst cartridge (411b) serves to bond the carbon component contained in the water in the mixed oil and the hydrogen component contained in the oil. Illustratively, the carbon component contained in the water in the mixed oil may be ionized carbon that has passed through the first ionization catalyst cartridge (411a). Further, the hydrogen component contained in the oil of the mixed oil may be hydrogen ionized by pretreating the oil via the oil tank catalyst described above.
第3イオン化触媒カートリッジ(411c)は、第1イオン化触媒カートリッジ(411a)と第2イオン化触媒カートリッジ(411b)とを通過した混合油を安定化させる役割をする。 The third ionization catalyst cartridge (411c) serves to stabilize the mixed oil that has passed through the first ionization catalyst cartridge (411a) and the second ionization catalyst cartridge (411b).
つまり、混合油は、これらのイオン化触媒部(400)を経て、バイオエマルジョン燃料に生成される。 That is, the mixed oil is produced as a bioemulsion fuel via these ionization catalyst parts (400).
以下では、図6を参照して、本願の実施例による植物油を用いたバイオエマルジョン燃料の製造方法(以下、「本改質燃料の製造方法」という。)について説明する。 Hereinafter, a method for producing a bioemulsion fuel using vegetable oil according to the embodiment of the present application (hereinafter, referred to as “method for producing the reformed fuel”) will be described with reference to FIG.
本バイオエマルジョン燃料の製造方法は、オイルタンク部(100)内に供給されたオイルを凝集剤と遠心分離型デカンタを利用して精製された油を準備する段階(S10)を含む。 The method for producing the bioemulsion fuel includes a step (S10) of preparing refined oil by using a flocculant and a centrifuge decanter for the oil supplied into the oil tank portion (100).
また、本バイオエマルジョン燃料の製造方法は、水タンク部(200)内に供給された水を水タンク触媒により前処理して、前処理された水を準備する段階(S20)を含む。 In addition, the method for producing the bioemulsion fuel includes a step (S20) of preparing the pretreated water by pretreating the water supplied into the water tank section (200) with a water tank catalyst.
S20段階で、水タンク触媒はトルマリン光油を含む第1の水タンク触媒剤と、二酸化ケイ素、ケイ酸塩光油とハロゲン化光油いずれかを含む第2水タンク触媒剤と、を含む。 At the S20 stage, the water tank catalyst comprises a first water tank catalyst containing tourmaline light oil and a second water tank catalyst containing either silicon dioxide, silicate light oil or halogenated light oil.
また、本バイオエマルジョン燃料の製造方法は、混合油生成部(300)内で、オイルタンク部(100)から流入した精製された油と水タンク部(200)から流入した前処理された水を攪拌して混合油を形成する段階(S30)を含む。 Further, in the method for producing this bioemulsion fuel, in the mixed oil generating section (300), the refined oil flowing from the oil tank section (100) and the pretreated water flowing from the water tank section (200) are used. Including the step (S30) of stirring to form a mixed oil.
混合油生成部(300)内で油と水はそれぞれが分離されず、均一に物理的に混合された混合油が形成されることができる。 Oil and water are not separated from each other in the mixed oil generating section (300), and a uniformly physically mixed mixed oil can be formed.
また、本バイオエマルジョン燃料の製造方法は、イオン化触媒部(400)内で、混合油生成部(300)から流入した混合油をイオン化触媒を用いて、最終的バイオエマルジョン燃料を生成する段階(S40)を含む。 In addition, the method for producing this bioemulsion fuel is a stage (S40) in which the mixed oil flowing from the mixed oil generation unit (300) is used in the ionization catalyst unit (400) to produce the final bioemulsion fuel using the ionization catalyst. )including.
前述のように、イオン化触媒は、イオン化触媒部(400)に備えられることができる。また、イオン化触媒部(400)は、複数のイオン化触媒群(410)を含む。そして、それぞれのイオン化触媒群(410)は、複数のイオン化触媒カートリッジ(411)を含む。 As described above, the ionization catalyst can be provided in the ionization catalyst unit (400). Further, the ionization catalyst unit (400) includes a plurality of ionization catalyst groups (410). Each ionization catalyst group (410) includes a plurality of ionization catalyst cartridges (411).
前述した本明細書の説明は、例示のためのものであり、本明細書が属する技術分野の通常の知識を有する者は、本明細書の技術や特徴を変更せず、他の具体的な形で容易に変形が可能であることを理解できると思量する。したがって、以上で記述した実施例は、すべての面で例示的なものであり限定ではない事を理解されたい。例えば、単一型で説明されている各コンポーネントは、分散され、実施されることもあり、同様に分散されたものと説明されている構成要素も結合された形態で実施することもある。 The above description of the present specification is for illustrative purposes only, and a person having ordinary knowledge of the technical field to which the present specification belongs does not change the technology or features of the present specification, and other specifics. I think you can understand that the shape can be easily deformed. Therefore, it should be understood that the examples described above are exemplary in all respects and not limited. For example, each component described as a single type may be distributed and implemented, and components described as similarly distributed may also be implemented in a combined form.
本願の範囲は、上記の詳細な説明ではなく、後述する特許請求の範囲によって示され、特許請求の範囲の意味及び範囲、そしてその均等概念から導き出されるすべての変更または変形された形態が本明細書の範囲に含まれるものと解釈されるべきである。 The scope of the present application is shown not by the above detailed description but by the scope of claims described later, and the meaning and scope of the claims and all modified or modified forms derived from the concept of equality thereof are described herein. It should be interpreted as being included in the scope of the book.
10:植物性原料を使用したバイオエマルジョン燃料製造装置
100:オイルタンク部
110:オイル供給ポンプ
120:オイルタンク
130:凝集剤投入機
140:オイル移送ポンプ
150:遠心分離型デカンタ
160:オイル収集タンク
170:精製オイルタンク
180:精製オイル移送ポンプ
200:水タンク部
210:給水ポンプ
220:水タンク
300:混合油生成部
310:高圧オイル移送ポンプ
320:高圧水移送ポンプ
330:開閉弁
340:流量計
350:圧力計
360:インラインミキサー
370:混合油タンク
400:イオン化触媒部
405:混合油移送ポンプ
406:開閉弁
410:イオン化触媒群
10: Bioemulsion fuel production equipment using vegetable raw materials
100: Oil tank
110: Oil supply pump
120: Oil tank
130: Coagulant input machine
140: Oil transfer pump
150: Centrifugal decanter
160: Oil collection tank
170: Refined oil tank
180: Refined oil transfer pump
200: Water tank
210: Water supply pump
220: Water tank
300: Mixed oil generator
310: High pressure oil transfer pump
320: High pressure water transfer pump
330: On-off valve
340: Flow meter
350: Pressure gauge
360: In-line mixer
370: Mixed oil tank
400: Ionization catalyst section
405: Mixed oil transfer pump
406: On-off valve
410: Ionization catalyst group
このとき、水タンク触媒はトルマリン原石のようなトルマリン鉱物を含む第1の水タンク触媒、及び二酸化ケイ素、ケイ酸塩の鉱物とハロゲン化鉱物のいずれかを含む第2の水タンク触媒を含むことができる。 At this time, the water tank catalyst includes a first water tank catalyst containing a tourmaline mineral such as tourmaline rough, and a second water tank catalyst containing either silicon dioxide, a silicate mineral or a halide mineral. Can be done.
例示的に、第2の水タンク触媒は二酸化ケイ素、ケイ酸塩の鉱物とハロゲン化鉱物を含む矩形の触媒として利用されることができる。ここで、矩形の触媒は、約1cmの直径を持つことができる。 Illustratively, the second water tank catalyst can be utilized as a rectangular catalyst containing silicon dioxide, silicate minerals and halide minerals . Here, the rectangular catalyst can have a diameter of about 1 cm.
S20段階で、水タンク触媒はトルマリン鉱物を含む第1の水タンク触媒剤と、二酸化ケイ素、ケイ酸塩鉱物とハロゲン化鉱物いずれかを含む第2水タンク触媒剤と、を含む。 In step S20, the water tank catalyst comprises a first water tank catalytic agents containing tourmaline mineral, silicon dioxide, and the second water tank catalytic agent containing either silicate minerals and halogenated minerals, the.
Claims (13)
流入した植物油の不純物を除去し、精製されたオイルを保存するオイルタンク部;
流入した水を水タンク触媒を利用して前処理する水タンク部;
前記オイルタンク部と水タンク部とに接続されて、オイルタンク部から流入した精製されたオイルと水タンク部から流入した前処理された水とを物理的に攪拌して混合油を製造する、混合油生成部;及び、
オイル供給ポンプで移送されたオイルを一時的に保存する混合油生成部と接続されて、混合油生成部から流入した混合油をイオン化触媒を利用して、バイオエマルジョン燃料を生成するイオン化触媒部を含むことを特徴とする植物油を利用したバイオエマルジョン燃料製造装置。 In a bioemulsion fuel production device using vegetable oil
Oil tank section that removes impurities from the inflowing vegetable oil and stores the refined oil;
Water tank part that pretreats the inflowing water using a water tank catalyst;
A mixed oil is produced by being connected to the oil tank portion and the water tank portion and physically stirring the refined oil flowing from the oil tank portion and the pretreated water flowing from the water tank portion. Mixed oil generator; and
An ionization catalyst unit that is connected to a mixed oil generator that temporarily stores the oil transferred by the oil supply pump and uses an ionization catalyst to generate bioemulsion fuel from the mixed oil that has flowed in from the mixed oil generator. A bioemulsion fuel production device using vegetable oil, which is characterized by containing.
流入したオイルを移送するオイル供給ポンプ;
オイルタンク;
前記オイルタンクの上部に接続されてオイル内の不純物を凝集させる凝集剤を投与する凝集剤投入機;
前記オイルタンク内のオイルや不純物を移送させるオイル移送ポンプ;
前記オイル移送ポンプによって移送されたオイルの不純物を凝固させて分離排出し精製されたオイルだけを生成させる遠心分離型デカンタ;
精製されたオイルを移送させる精製油移送ポンプ;及び
精製されたオイルを一時的に保存する精製油タンクを含むことを特徴とする請求項1に記載の植物油を利用したバイオエマルジョン燃料製造装置。 The oil tank portion is further
Oil supply pump that transfers the inflowing oil;
Oil tank;
A flocculant input machine that is connected to the upper part of the oil tank and administers a flocculant that aggregates impurities in the oil;
An oil transfer pump that transfers oil and impurities in the oil tank;
Centrifugal decanter that coagulates impurities in the oil transferred by the oil transfer pump, separates and discharges them, and produces only refined oil;
The bioemulsion fuel production apparatus using a vegetable oil according to claim 1, further comprising a refined oil transfer pump for transferring the refined oil; and a refined oil tank for temporarily storing the refined oil.
トルマリン光油を含む第1の水タンク触媒剤;及び
二酸化ケイ素、ケイ酸塩光油、及びハロゲン化光油のいずれかを含む第2の水タンク触媒剤を含むことを特徴とする請求項1に記載の植物油を利用したバイオエマルジョン燃料製造装置。 The water tank catalyst is
Claim 1 comprising a first water tank catalyst comprising tourmaline light oil; and a second water tank catalyst comprising any of silicon dioxide, silicate light oil, and halogenated light oil. A bioemulsion fuel production device using the vegetable oil described in 1.
前処理された前記水を高圧で移送させる高圧水移送ポンプによる移送で、精製された前記オイルと前処理された前記水のラインを一つに合わせ、物理的に混合させるY字型のインラインミキサー;及び、
混合油を一時的に保存する混合油タンクを含むことを特徴とする請求項1に記載の植物油を利用したバイオエマルジョン燃料製造装置。 The mixed oil generator is a high-pressure oil transfer pump that transfers the refined oil at high pressure;
A Y-shaped in-line mixer that physically mixes the refined oil and the pretreated water lines by transferring them with a high-pressure water transfer pump that transfers the pretreated water at high pressure. ;as well as,
The bioemulsion fuel production apparatus using a vegetable oil according to claim 1, further comprising a mixed oil tank for temporarily storing the mixed oil.
前記高圧水移送ポンプと前記インラインミキサーとの間のラインには、前処理された前記水の流量を制御することができる開閉弁、前処理された前記水の圧力を測定する圧力計、及び前処理された前記水の量を測定する流量計を含むことを特徴とする請求項4に記載の植物油を利用したバイオエマルジョン燃料製造装置。 The line between the high pressure oil transfer pump and the in-line mixer includes an on-off valve that can control the flow rate of the refined oil, a pressure gauge that measures the pressure of the refined oil, and refined oil. A flow meter is provided to measure the amount of oil.
The line between the high-pressure water transfer pump and the in-line mixer includes an on-off valve capable of controlling the flow rate of the pretreated water, a pressure gauge for measuring the pressure of the pretreated water, and a pretreated water. The bioemulsion fuel production apparatus using vegetable oil according to claim 4, further comprising a flow meter for measuring the amount of the treated water.
複数のイオン化触媒群;
を備えており、
前記複数のイオン化触媒群は、前記混合油を順次通過させる複数のイオン化触媒カートリッジを有する少なくとも一つ以上のイオン化の触媒群を含み、
前記イオン化触媒カートリッジには、前記イオン化触媒が配置されるものであることを特徴とする請求項1に記載の植物油を利用したバイオエマルジョン燃料製造装置。 The ionization catalyst unit is a mixed oil transfer pump that transfers mixed oil from a mixed oil tank; and a plurality of ionization catalyst groups;
Is equipped with
The plurality of ionization catalyst groups include at least one or more ionization catalyst groups having a plurality of ionization catalyst cartridges through which the mixed oil is sequentially passed.
The bioemulsion fuel production apparatus using vegetable oil according to claim 1, wherein the ionization catalyst is arranged in the ionization catalyst cartridge.
前記混合油内の水に含まれている炭素のイオン化を引き起こす第1イオン化触媒カートリッジ;
前記混合油内の水に含まれる炭素成分と、前記混合油の油に含まれる水素の成分の結合を誘導する第2イオン化触媒カートリッジ;及び
前記第1イオン化触媒カートリッジと前記第2イオン化触媒カートリッジとを通過した混合油を安定化させてくれる第3イオン化触媒カートリッジ;
を含むものであることを特徴とする請求項9に記載の植物油を利用したバイオエマルジョン燃料製造装置。 Each of the multiple ionization catalyst cartridges
The first ionization catalyst cartridge that causes the ionization of carbon contained in the water in the mixed oil;
The second ionization catalyst cartridge that induces the bond between the carbon component contained in the water in the mixed oil and the hydrogen component contained in the oil of the mixed oil; and the first ionization catalyst cartridge and the second ionization catalyst cartridge. A third ionization catalyst cartridge that stabilizes the mixed oil that has passed through the
The bioemulsion fuel production apparatus using the vegetable oil according to claim 9, which comprises the above.
オイルタンク部内に供給されたオイルを凝集剤と遠心分離型デカンタとを使用して、不純物を除去した精製された油を準備する段階;
水タンク部内に供給された水を水タンク触媒により前処理して、前処理された水を準備する段階;
混合油生成部内で、前記のオイルタンク部から流入した精製された前記オイルと前記水タンク部から流入した前処理された前記水を攪拌して混合油を形成する段階;及び、
イオン化触媒部内で、前記混合油生成部から流入した前記混合油をイオン化触媒を用いて、バイオエマルジョン燃料を生成する段階を含んでいる植物油を利用したバイオエマルジョン燃料の製造方法。 A method for producing bioemulsion fuel using vegetable oil.
The stage of preparing refined oil from which impurities have been removed by using a flocculant and a centrifuge decanter for the oil supplied into the oil tank section;
The stage where the water supplied into the water tank is pretreated with a water tank catalyst to prepare the pretreated water;
In the mixed oil generation section, a step of stirring the refined oil flowing from the oil tank section and the pretreated water flowing from the water tank section to form a mixed oil;
A method for producing a bioemulsion fuel using a vegetable oil, which comprises a step of producing a bioemulsion fuel by using an ionization catalyst for the mixed oil flowing from the mixed oil generation unit in the ionization catalyst unit.
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